Classifications

• • C—CHEMISTRY; METALLURGY
  • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
  • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
  • C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
  • C22B3/18—Extraction of metal compounds from ores or concentrates by wet processes with the aid of microorganisms or enzymes, e.g. bacteria or algae
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P10/00—Technologies related to metal processing
  • Y02P10/20—Recycling

Definitions

• This invention relates generally to a tank bioleaching process and more particularly is concerned with the supply of carbon to microbial cells used in a tank bioleaching process.
• the tank or reactor contains a slurry of the concentrate which is agitated and to which nutrients are added.
• the slurry is sparged with air or enriched air and its pH is controlled usually in the range of 0.8 - 2 pH.
• the microbial cells which are used in this type of bioleaching process are usually chemolithrophs and grow autotrophically by fixing carbon dioxide, from the atmosphere or in a supplied gas phase, in order to satisfy their carbon requirements. Microbial cells require carbon as a fundamental component of cellular metabolites and functional products. INT1157/MAJR/jes 2
• thermophilic bioleaching above 45 0 C
• the use of enriched air is important due to the reduced solubility and resulting reduced mass transfer of CO2 and oxygen with an increase in temperature.
• the enriched air may contain an elevated concentration of oxygen or carbon dioxide for it is well documented that such elevated concentrations are required in order to achieve optimal microbial growth and ferrous and sulphur oxidation rates.
• the oxygen and carbon dioxide required to enrich the air which is sparged into the reactor are normally produced by generation plants.
• the capital and operating costs of these plants are however significant with the cost associated with carbon dioxide being particularly expensive.
• the utilization percentage of supplied carbon dioxide during a bioleaching process can be low, often less than 40%. This adds materially to the cost of operating a bioleaching plant.
• the concentrate material that is subjected to bioleaching contains silver, in addition to the metal of interest, usually copper, nickel or gold.
• the presence of silver may in certain instances result in severe inhibitory effects towards microbial cells, and thus negatively affect the bioleaching process.
• silver is only sparingly soluble under typical bioleaching conditions, dissolution of the mineral in which silver is contained results in the transient presence of silver in solution before complexation and precipitation occurs in the reactor.
• Such transient solubility is sufficient to result in rapid interaction of silver with microbial cells, where the silver most commonly penetrates the cell membrane and binds, with high affinity, to compounds contained in the cellular cytoplasm.
• the compounds with which silver is most likely to INT1157/MAJR/jes 3 interact in the cell are the sulphur-containing amino acids cysteine and methionine, amongst other Silver inhibitory effects can readily be observed by transmission electron microscopy, in conjunction with metal analysis techniques, as the presence of silver nodules inside affected cells
• the invention provides a method of operating a tank bioleaching process of a concentrate, which includes the step of supplying carbon in a non-gaseous form to microbial cells used in the process This results in lower carbon costs and has the unexpected benefit of reducing the inhibitory effect of silver toward the microbial cells
• Carbon which is supplied to the process in the aforementioned manner can be in place of, or in addition to, carbon which is supplied to the process in the form of carbon dioxide
• Any appropriate source can be used for supplying carbon in a non-gaseous form
• the source may be selected from water-soluble carbon and inorganic carbonaceous solid compounds such as carbonates
• the carbon is derived from an organic soluble carbon which may be selected from yeast, a yeast extract, and carbon extracts or carbon derived from activated sludge, tannery effluents, spent bioleaching biomass, molasses, corn steep liquor, sucrose, glucose and methanol INT1157/MAJR/jes 4
• Yeast extract is a preferred carbon source for it usually contains a number of nutritional compounds such as vitamins, amino acids, and co-factors, in addition to carbon, which promote microbial growth. Similar compounds include meat extract. Such complex nutritional compounds way be used on their own or in conjunction with pure carbon sources. The aim of using such mixtures (as yeast extract) would be to replace at least the carbon supplied by the complex nutritional source, and thus reduce the overall consumption of the yeast extract.
• Complex nutritional sources such as yeast extract contain a large variety of other nutritional compounds in addition to carbon. Amongst these are compounds with a high affinity for complexing silver from solution. These compounds are thought to be sulphur- containing amino acids, but may also include other currently unknown compounds. The unexpected benefit is that these compounds act by rapidly scavenging silver from the dissolved state, thus preventing and/or reducing the detrimental interaction of silver with the microbial or bioleaching cells. This mechanism facilitates a more robust bioleaching process for ores containing silver that would otherwise prohibit the processing of such ores by biohydrometallurgical means.
• sucrose can be used in combination with complex nutrients sources (such as yeast extract).
• complex nutrients sources such as yeast extract.
• sucrose has been found to have a unexpected benefit in such applications as it seems to increase the cell membrane robustness, stability and integrity under the harsh bioleaching conditions. This is beneficial from an operation process point of view. INT1157/MAJR/jes 5
• FIG. 1 The accompanying drawing illustrates, somewhat schematically, a tank bioleaching process 10
• a slurry 12 which contains mineral concentrates milled to a small particle size, typically less than 80 micrometers, is directed to a reactor or tank 14 which includes a motor driven impeller 16 used for agitating the slurry
• the slurry is inoculated with known bacteria and, optionally, nutrients 18 are supplied to the slurry in the reactor in accordance with known criteria
• Gas 20 is supplied to a sparging system 22 in the reactor
• the gas may be air which is enriched with oxygen 24 and, optionally, carbon dioxide 26, according to requirement
• the slurry in the reactor is kept at a desired pH level and at a desired temperature, in accordance with known criteria, so that the bioleaching process decomposes or solubilises the target metals which are subsequently recovered in a downstream process 28
• bioleaching microorganisms have an obligate requirement for carbon dioxide as their sole source of carbon although some strains, e.g. facultative autotrophic and facultative heterotrophic, are less peremptory in this respect. Such strains are thus able to use carbon sources other than carbon dioxide either as a substitute for the carbon dioxide or as a supplement to the carbon dioxide. It is thus possible to achieve an optimal tank bioleaching condition by supplying a water-soluble organic carbon source, such as a yeast extract 32, to the tank.
• a water-soluble organic carbon source such as a yeast extract 32
• the carbon source is preferably supplied in liquid form and is pumped into the reactor 14 or, as is indicated by a dotted INT1157/MAJR/jes 7 line, into the slurry feed 12 or, alternatively or additionally, is added as a dry powder to the slurry in the tank.
• the non-gaseous carbon is maintained in the reactor at a concentration which may lie in the range of from 10 to 600 mg/L although, according to requirement, higher or lower concentrations of the carbon source material may prevail in the slurry.
• yeast extract is a product which is produced by methods, known in the art, that include a lysis step (i.e. rupturing of the cells), thus releasing the contents of the cells.
• the water-soluble cell content is separated from the cell particulates and is produced either as a paste or as a dry water-soluble powder.
• the final product, known as yeast extract contains a high concentration and variety of amino acids, vitamins, and organic and inorganic nutrients and is therefore suitable for use in microbial growth media.
• the yeast extract can often be obtained at a lower cost, measured on carbon content, than CO 2 . Also, the utilisation of carbon in the yeast, by the microbial cells, is more effective (i.e. more carbon is used) than when the carbon is presented in gaseous form i.e. as CO 2 . The use of yeast extract with pure carbon sources such as sucrose, may reduce the overall cost of such carbon supplementation.
• soluble carbon sources suitable for use in the invention, are carbon compounds that are purified to a level where the main constituent compound dominates and can be readily identified, such as sucrose, glucose and methanol.
• a water-soluble carbon source such as a yeast extract (complex nutritional source) alone or in combination with sucrose (a pure carbon source)
• sucrose a pure carbon source

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• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Life Sciences & Earth Sciences (AREA)
• Manufacturing & Machinery (AREA)
• Mechanical Engineering (AREA)
• Microbiology (AREA)
• Environmental & Geological Engineering (AREA)
• General Life Sciences & Earth Sciences (AREA)
• Geochemistry & Mineralogy (AREA)
• Geology (AREA)
• Biochemistry (AREA)
• Materials Engineering (AREA)
• Biotechnology (AREA)
• Metallurgy (AREA)
• Organic Chemistry (AREA)
• Micro-Organisms Or Cultivation Processes Thereof (AREA)
• Preparation Of Compounds By Using Micro-Organisms (AREA)
• Manufacture And Refinement Of Metals (AREA)
• Enzymes And Modification Thereof (AREA)
• Apparatus Associated With Microorganisms And Enzymes (AREA)

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Citations (4)

• 2005
  • 2005-07-08 AU AU2005265429A patent/AU2005265429A1/en not_active Abandoned
  • 2005-07-08 EP EP05776059A patent/EP1789599B1/en not_active Not-in-force
  • 2005-07-08 WO PCT/ZA2005/000104 patent/WO2006010170A1/en active Application Filing
  • 2005-07-08 CN CNB2005800244715A patent/CN100478464C/zh not_active Expired - Fee Related
  • 2005-07-08 CA CA002574240A patent/CA2574240A1/en not_active Abandoned
  • 2005-07-08 AP AP2007003874A patent/AP2295A/xx active
  • 2005-07-08 ES ES05776059T patent/ES2313398T3/es active Active
  • 2005-07-08 EA EA200700272A patent/EA013548B1/ru not_active IP Right Cessation
  • 2005-07-08 AT AT05776059T patent/ATE406465T1/de not_active IP Right Cessation
  • 2005-07-08 PL PL05776059T patent/PL1789599T3/pl unknown
  • 2005-07-08 DE DE602005009376T patent/DE602005009376D1/de not_active Expired - Fee Related
  • 2005-07-15 AR ARP050102944A patent/AR050081A1/es active IP Right Grant
  • 2005-07-18 PE PE2005000828A patent/PE20060543A1/es not_active Application Discontinuation
• 2006
  • 2006-12-21 ZA ZA200610842A patent/ZA200610842B/xx unknown
• 2007
  • 2007-01-15 US US11/623,166 patent/US20070172935A1/en not_active Abandoned

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